Method for preparing graft copolymers and compositions produced therefrom

ABSTRACT

An aqueous polymerization method for preparing graft copolymers is disclosed. Copolymer compositions produced therefrom are also disclosed. The method of the present invention includes (a) forming a macromonomer aqueous emulsion containing water insoluble macromonomer particles; (b) forming a monomer composition containing at least one ethylenically unsaturated monomer; and (c) combining at least a portion of the macromonomer aqueous emulsion and at least a portion of the monomer composition and polymerizing the resulting polymerization reaction mixture in the presence of an initiator to form a copolymer composition. The copolymer composition produced contains water insoluble particles of graft copolymer.

[0001] This application is a division of Ser. No. 09/951,494 filed Sep.13, 2001, which derives priority from provisional patent applicationSerial No. 60/232,414 filed Sep. 14, 2000.

FIELD OF INVENTION

[0002] This invention relates to a method for making graft copolymersusing an aqueous emulsion polymerization process, and copolymercompositions produced therefrom. More particularly, this inventionrelates to an aqueous emulsion polymerization process for polymerizingat least one macromonomer and at least one ethylenically unsaturatedmonomer to form a copolymer composition containing graft copolymers.

BACKGROUND OF THE INVENTION

[0003] “Graft copolymers” as used herein are macromolecules formed whenpolymer or copolymer chains are chemically attached as side chains to apolymeric backbone. Generally, the side chains are of a differentpolymeric composition than the backbone chain. Because graft copolymersoften chemically combine unlike polymeric segments in one molecule,these copolymers have unique properties compared to the correspondingrandom analogues. These properties include, for example, mechanical filmproperties resulting from thermodynamically driven microphase separationof the polymer, and decreased melt viscosities resulting in part fromthe branched structure of the graft copolymer. With respect to thelatter, reduced melt viscosities can advantageously improveprocessability of the polymer. See e.g., Hong-Quan Xie and Shi-BiaoZhou, J. Macromol. Sci.-Chem., A27(4), 491-507 (1990); Sebastian Roos,Axel H. E. Müller, Marita Kaufmann, Werner Siol and Clenens Auschra,“Applications of Anionic Polymerization Research”, R. P. Quirk, Ed., ACSSymp. Ser. 696, 208 (1998).

[0004] The term “comb copolymer,” as used herein, is a type of graftcopolymer, where the polymeric backbone of the graft copolymer islinear, and each side chain of the graft copolymer is formed by a“macromonomer” that is grafted to the polymer backbone. “Macromonomers”are low molecular weight polymers having at least one functional groupat the end of the polymer chain that can further polymerize with othersmonomers to yield comb copolymers. See e.g., Kawakami in the“Encyclopedia of Polymer Science and Engineering”, Vol. 9, pp. 195-204,John Wiley & Sons, New York, 1987. The term “linear,” as used herein, ismeant to include polymers where minor amounts of branching has occurredthrough hydrogen abstraction that is normally observed in free radicalpolymerizations. The comb copolymers are commonly prepared by the freeradical copolymerization of macromonomer with conventional monomer(e.g., ethylenically unsaturated monomers).

[0005] Comb copolymers prepared with water-insoluble macromonomers havebeen predominantly prepared using bulk and solution polymerizationtechniques. However, such processes undesirably use solvent or monomeras the medium in which the polymerization is conducted. Thus, effortsrecently have focused on developing methods for preparing combcopolymers via an aqueous emulsion process.

[0006] One example, U.S. Pat. No. 5,247,040 to Amick et al., (“Amick”),discloses a two stage emulsion polymerization process for producinggraft copolymers. In the first stage, a macromonomer is produced bypolymerizing ethylenically unsaturated monomer in the presence of amercapto-olefin compound. In the second stage, the resultingmacromonomer is polymerized in an aqueous emulsion with a secondethylenically unsaturated monomer. The Amick process, although havingmany advantages, produces a graft copolymer having linkages, locatedbetween the side chains and backbone, that are susceptible to hydrolysisunder certain conditions. These linkages result from using amercapto-olefin compound having an ester functionality in thepreparation of the macromonomer.

[0007] U.S. Pat. No. 5,264,530 to Darmon et al. (“Darmon”) discloses anemulsion or suspension free radical polymerization process where one ormore monomer species is polymerized in the presence of a macromonomerthat is used as a chain transfer agent. As the macromonomer is beingused as a chain transfer agent, the macromonomer is predominatelyincorporated into the polymer chain at the ends.

[0008] U.S. Pat. No. 5,804,632 to Haddleton et al. (“Haddleton”)discloses an aqueous polymer emulsion process that includes preparing,in the presence of a cobalt chelate complex, a low molecular weightpolymer having acid functional groups, and subsequently polymerizing atleast one olefinically unsaturated monomer in the presence of the lowmolecular weight polymer to form a hydrophobic polymer. The lowmolecular weight polymer in Haddleton is taught to contain a sufficientconcentration of acid to render the low molecular weight polymer, as is,or upon neutralization of the acid groups, partially or more preferablyfully dissolvable in an aqueous medium. Although Haddleton disclosesthat some degree of grafting may occur, Haddleton focuses on processeswhere it is believed that the hydrophobic polymer particles areencapsulated by the low molecular weight polymer in the form of an“inverted core-shell” latex, or where the low molecular weight polymerserves simply as a seed for the polymerization to form the hydrophobicpolymer. Thus, Haddleton does not disclose a process to produce graftcopolymers of a desired structure such as comb copolymers. It is alsobelieved that using the Haddleton process undesirably results in asubstantial amount of low molecular weight polymer remaining unreactedin the water phase.

[0009] Publication WO 99/03905 to Huybrechts et al. (“Huybrechts”)discloses an anionically stabilized graft copolymer composition that isprepared by emulsion polymerizing acid containing macromonomer and aminofunctional monomer. The copolymer composition prepared contains from 0.5to 30 weight percent amino functional monomer in the polymer backbone,and at least 5 weight percent acid functional monomer in themacromonomer that is neutralized with an amine. However, it would bedesirable to provide an aqueous emulsion polymerization process forpreparing alternative graft copolymer compositions that do not requireneutralization.

[0010] The present invention seeks to provide a robust emulsionpolymerization process for preparing graft copolymers that arepreferably resistant to hydrolysis. The present invention also seeks toprovide an emulsion polymerization process that preferably providescontrol over such parameters as polymerization kinetics, polymerstructure, conversion, incorporation of macromonomer and particle size.

SUMMARY OF INVENTION

[0011] In one aspect of the present invention, a method of making agraft copolymer is provided that includes forming a macromonomer aqueousemulsion containing water-insoluble particles of macromonomer andforming a monomer composition containing ethylenically unsaturatedmonomer. The macromonomer contains polymerized units of a firstethylenically unsaturated monomer and further has a degree ofpolymerization of from 10 to 1000, at least one terminal ethylenicallyunsaturated group, less than 5 weight percent acid-containing monomer aspolymerized, and less than 1 mole percent of mercapto-olefin compoundsas polymerized. At least a portion of the macromonomer aqueous emulsionand at least a portion of the monomer composition are combined to form apolymerization reaction mixture, and the macromonomer and the secondethylenically unsaturated monomer therein are polymerized in thepresence of an initiator to produce a graft copolymer compositioncontaining graft copolymer particles.

[0012] In another aspect of the present invention, a graft copolymercomposition is provided that contains water insoluble graft copolymerparticles. The copolymer particles contain from 2 weight percent to 90weight percent water insoluble macromonomer, and from 10 weight percentto 98 weight percent of polymerized units of at least one secondethylenically unsaturated monomer, based on the total weight of thecopolymer. The macromonomer used to form the graft copolymer compositioncontains from 10 to 1000 polymerized units of a first ethylenicallyunsaturated monomer, less than 1 mole percent of polymerizedmercapto-olefin compounds, and less than 5 weight percent polymerizedacid-containing monomer. In a preferred embodiment, the copolymercomposition further contains from 0.2 weight percent to 10 weightpercent of an acid containing macromonomer, based on the total weight ofthe copolymer.

DETAILED DESCRIPTION

[0013] The present invention provides an aqueous polymerization processfor preparing graft copolymers, and more preferably comb copolymers. Thepresent invention also provides novel copolymer compositions producedfrom the aqueous polymerization process.

[0014] The process of the present invention includes (a) forming amacromonomer aqueous emulsion containing one or more water-insolubleparticles of macromonomer; (b) forming a monomer composition containingethylenically unsaturated monomer; and (c) combining at least a portionof the macromonomer aqueous emulsion and at least a portion of themonomer composition to form a polymerization reaction mixture. Themacromonomer and ethylenically unsaturated monomer are polymerized inthe presence of an initiator to form graft copolymer particles.

[0015] The macromonomer, present in the macromonomer aqueous emulsion aswater insoluble particles, is any low molecular weight water-insolublepolymer or copolymer having at least one terminal ethylenicallyunsaturated group that is capable of being polymerized in a free radicalpolymerization process. By “water-insoluble” it is meant having a watersolubility of no greater than 150 millimoles/liter at 25° C. to 50° C.By “low molecular weight” it is meant that the macromonomer has a degreeof polymerization preferably from about 10 to about 1000, and morepreferably from about 20 to about 200. By “degree of polymerization” itis meant the number of polymerized monomer units present in themacromonomer.

[0016] The macromonomer contains, as polymerized units, at least onetype of ethylenically unsaturated monomer. Preferably, the ethylenicallyunsaturated monomer is selected to impart low or no water solubility tothe macromonomer as previously described herein.

[0017] Suitable ethylenically unsaturated monomers for use in preparingmacromonomer include for example methacrylate esters, such as C₁ to C₁₈normal or branched alkyl esters of methacrylic acid, including methylmethacrylate, ethyl methacrylate, n-butyl methacrylate, laurylmethacrylate, stearyl methacrylate; acrylate esters, such as C₁ to C₁₈normal or branched alkyl esters of acrylic acid, including methylacrylate, ethyl acrylate, n-butyl acrylate and 2-ethylhexyl acrylate;styrene; substituted styrenes, such as methyl styrene, α-methyl styreneor t-butyl styrene; olefinically unsaturated nitriles, such asacrylonitrile or methacrylonitrile; olefinically unsaturated halides,such as vinyl chloride, vinylidene chloride or vinyl fluoride; vinylesters of organic acids, such as vinyl acetate; N-vinyl compounds suchas N-vinyl pyrrolidone; acrylamide; methacrylamide; substitutedacrylamides; substituted methacrylamides; hydroxyalkylmethacrylates suchas hydroxyethylmethacrylate; hydroxyalkylacrylates; basic substituted(meth)acrylates and (meth)acrylamides, such as amine-substitutedmethacrylates including dimethylaminoethyl methacrylate,tertiary-butylaminoethyl methacrylate and dimethylaminopropylmethacrylamide and the likes; dienes such as 1,3-butadiene and isoprene;vinyl ethers; or combinations thereof. The term “(meth)” as used hereinmeans that the “meth” is optionally present. For example,“(meth)acrylate” means methacrylate or acrylate.

[0018] The ethylenically unsaturated monomer can also be a functionalmonomer including for example monomers containing hydroxy, amido,aldehyde, ureido, polyether, glycidylalkyl, keto functional groups orcombinations thereof. These functional monomers are generally present inthe macromonomer at a level of from about 0.5 weight percent to about 15weight percent and more preferably from about 1 weight percent to about3 weight percent, based on the total weight of the graft copolymer.Examples of functional monomers include ketofunctional monomers such asthe acetoacetoxy esters of hydroxyalkyl acrylates and methacrylates(e.g., acetoacetoxyethyl methacrylate) and keto-containing amides (e.g.,diacetone acrylamide); allyl alkyl methacrylates or acrylates;glycidylalkyl methacrylates or acrylates; or combinations thereof. Suchfunctional monomer can provide crosslinking if desired.

[0019] The macromonomer also contains as polymerized units less thanabout 10 weight percent, preferably less than about 5 weight percent,more preferably less than 2 weight percent and most preferably less thanabout 1 weight percent acid containing monomer, based on the totalweight of the macromonomer. In a most preferred embodiment, themacromonomer contains no acid containing monomer. By “acid containingmonomer” it is meant any ethylenically unsaturated monomer that containsone or more acid functional groups or functional groups that are capableof forming an acid (e.g., an anhydride such as methacrylic anhydride ortertiary butyl methacrylate). Examples of acid containing monomersinclude, for example, carboxylic acid bearing ethylenically unsaturatedmonomers such as acrylic acid, methacrylic acid, itaconic acid, maleicacid and fumaric acid; acryloxypropionic acid and(meth)acryloxypropionic acid; sulphonic acid-bearing monomers, such asstyrene sulfonic acid, sodium vinyl sulfonate, sulfoethyl acrylate,sulfoethyl methacrylate, ethylmethacrylate-2-sulphonic acid, or2-acrylamido-2-methylpropane sulphonic acid; phosphoethylmethacrylate;the corresponding salts of the acid containing monomer; or combinationsthereof.

[0020] The macromonomer also contains, as polymerized, less than about 1mole percent, preferably less than about 0.5 mole percent, and morepreferably no mercapto-olefin compounds, based on the total weight ofthe macromonomer. These mercapto-olefin compounds are those as describedin U.S. Pat. No. 5,247,000 to Amick, which is incorporated herein byreference in its entirety. The mercapto-olefin compounds described inAmick have ester functional groups, which are susceptible to hydrolysis.

[0021] In a preferred embodiment of the present invention, themacromonomer is composed of at least about 20 weight percent, morepreferably from about 50 weight percent to about 100 weight percent, andmost preferably from about 80 to about 100 weight percent of at leastone α-methyl vinyl monomer, a non α-methyl vinyl monomer terminated witha α-methyl vinyl monomer, or combinations thereof. In a most preferredembodiment of the present invention the macromonomer contains aspolymerized units from about 90 weight percent to about 100 weightpercent α-methyl vinyl monomers, non α-methyl vinyl monomers terminatedwith α-methyl vinyl monomers, or combinations thereof, based on thetotal weight of the macromonomer. Suitable α-methyl vinyl monomersinclude, for example, methacrylate esters, such as C₁ to C₁₈ normal orbranched alkyl esters of methacrylic acid, including methylmethacrylate, ethyl methacrylate, butyl methacrylate, 2-ethylhexylmethacrylate, isobornyl methacrylate, lauryl methacrylate, or stearylmethacrylate; hydroxyalkyl methacrylates such as hydroxyethylmethacrylate; glycidylmethacrylate; phenyl methacrylate; methacrylamide;methacrylonitrile; or combinations thereof. An example of a non α-methylvinyl monomer terminated with an α-methyl vinyl monomer includes styreneterminated by α-methyl styrene.

[0022] One skilled in the art will recognize that there are many ways toprepare the macromonomer useful in the present invention. For example,the macromonomer may be prepared by a high temperature (e.g., at leastabout 150° C.) continuous process such as disclosed in U.S. Pat. No.5,710,227 or EP-A-1,010,706, published Jun. 21, 2000, the disclosures ofwhich are hereby incorporated by reference in their entireties. In apreferred continuous process, a reaction mixture of ethylenicallyunsaturated monomers are passed through a heated zone having atemperature of at least about 150° C., and more preferably at leastabout 275° C. The heated zone may also be maintained at a pressure aboveatmospheric pressure (e.g., greater than about 30 bar). The reactionmixture of monomers may also optionally contain a solvent such as water,acetone, methanol, isopropanol, propionic acid, acetic acid,dimethylformamide, dimethylsulfoxide, methylethylketone, or combinationsthereof.

[0023] The macromonomer useful in the present invention may also beprepared by polymerizing ethylenically unsaturated monomers in thepresence of a free radical initiator and a catalytic metal chelate chaintransfer agent (e.g., a transition metal chelate). Such a polymerizationmay be carried out by a solution, bulk, suspension, or emulsionpolymerization process. Suitable methods for preparing the macromonomerusing a catalytic metal chelate chain transfer agent are disclosed infor example U.S. Pat. Nos. 4,526,945, 4,680,354, 4,886,861, 5,028,677,5,362,826, 5,721,330, and 5,756,605; European publicationsEP-A-0199,436, and EP-A-0196783; and PCT publications WO 87/03605, WO96/15158, and WO 97/34934, the disclosures of which are herebyincorporated by reference in their entireties.

[0024] Preferably, the macromonomer useful in the present invention isprepared by an aqueous emulsion free radical polymerization processusing a transition metal chelate complex. Preferably, the transitionmetal chelate complex is a cobalt (II) or (III) chelate complex such as,for example, dioxime complexes of cobalt, cobalt II porphyrin complexes,or cobalt II chelates of vicinal iminohydroxyimino compounds,dihydroxyimino compounds, diazadihydroxy-iminodialkyldecadienes, ordiazadihydroxyiminodialkylundecadienes, or combinations thereof. Thesecomplexes may optionally include bridging groups such as BF₂, and mayalso be optionally coordinated with ligands such as water, alcohols,ketones, and nitrogen bases such as pyridine. Additional suitabletransition metal complexes are disclosed in for example U.S. Pat. Nos.4,694,054; 5,770,665; 5,962,609; and 5,602,220, the disclosures of whichare hereby incorporated by reference in their entireties. A preferredcobalt chelate complex useful in the present invention is Co II(2,3-dioxyiminobutane-BF₂)₂, the Co III analogue of the aforementionedcompound, or combinations thereof. The spatial arrangements of suchcomplexes are disclosed in for example EP-A-199436 and U.S. Pat. No.5,756,605.

[0025] In preparing macromonomer by an aqueous emulsion polymerizationprocess using a transition metal chelate chain transfer agent, at leastone ethylenically unsaturated monomer is polymerized in the presence ofa free radical initiator and the transition metal chelate according toconventional aqueous emulsion polymerization techniques. Preferably, theethylenically unsaturated monomer is an α-methyl vinyl monomer aspreviously described herein.

[0026] The polymerization to form the macromonomer is preferablyconducted at a temperature of from about 20° C. to about 150° C., andmore preferably from about 40° C. to about 95° C. The solids level atthe completion of the polymerization is typically from about 5 weightpercent to about 65 weight percent, and more preferably from about 30weight percent to about 50 weight percent, based on the total weight ofthe aqueous emulsion.

[0027] The concentration of initiator and transition metal chelate chaintransfer agent used during the polymerization process is preferablychosen to obtain the desired degree of polymerization of themacromonomer. Preferably, the concentration of initiator is from about0.2 weight percent to about 3 weight percent, and more preferably fromabout 0.5 weight percent to about 1.5 weight percent, based on the totalweight of monomer. Preferably, the concentration of transition metalchelate chain transfer agent is from about 5 ppm to about 200 ppm, andmore preferably from about 10 ppm to about 100 ppm, based on the totalmoles of monomer used to form the macromonomer.

[0028] The ethylenically unsaturated monomer, initiator, and transitionmetal chelate chain transfer agent may be added in any manner known tothose skilled in the art to carry out the polymerization. For example,the monomer, initiator and transition metal chelate may all be presentin the aqueous emulsion at the start of the polymerization process(i.e., a batch process). Alternatively, one or more of the componentsmay be gradually fed to an aqueous solution (i.e., a continuous orsemi-batch process). For example, it may be desired to gradually feedthe entire or a portion of the initiator, monomer, and/or transitionmetal chelate to a solution containing water and surfactant. In apreferred embodiment, at least a portion of the monomer and transitionmetal chelate are gradually fed during the polymerization, with theremainder of the monomer and transition metal chelate being present inthe aqueous emulsion at the start of the polymerization. In thisembodiment, the monomer may be fed as is, or suspended or emulsified inan aqueous solution prior to being fed.

[0029] Any suitable free radical initiator may be used to prepare themacromonomer. The initiator is preferably selected based on suchparameters as its solubility in one or more of the other components(e.g., monomers, water); half life at the desired polymerizationtemperature (preferably a half life within the range of from about 30minutes to about 10 hours), and stability in the presence of thetransition metal chelate. Suitable initiators include for example azocompounds such as 2,2′-azobis (isobutyronitrile),4,4′-azobis(4-cyanovaleric acid), 2,2′-azobis[2-methyl-N-(1,1-bis(hydroxymethyl)-2-(hydroxyethyl)]-propionamide, and2,2′-azobis [2-methyl-N-(2-hydroxyethyl)]-propionamide; peroxides suchas t-butyl hydroperoxide, benzoyl peroxide; sodium, potassium, orammonium persulphate or combinations thereof. Redox initiator systemsmay also be used, such as for example persulphate or peroxide incombination with a reducing agent such as sodium metabisulphite, sodiumbisulfite, sodium formaldehyde sulfoxylate, isoascorbic acid, orcombinations thereof. Metal promoters, such as iron, may also optionallybe used in such redox initiator systems. Also, buffers, such as sodiumbicarbonate may be used as part of the initiator system.

[0030] An emulsifier is also preferably present during the aqueousemulsion polymerization process to prepare the macromonomer. Anyemulsifier may be used that is effective in emulsifying the monomerssuch as for example anionic, cationic, or nonionic emulsifiers. In apreferred embodiment, the emulsifier is anionic such as for examplesodium, potassium, or ammonium salts of dialkylsulphosuccinates; sodium,potassium, or ammonium salts of sulphated oils; sodium, potassium, orammonium salts of alkyl sulphonic acids, such as sodium dodecyl benzenesulfonate; sodium, potassium, or ammonium salts of alkyl sulphates, suchas sodium lauryl sulfate; ethoxylated alkyl ether sulfates; alkali metalsalts of sulphonic acids; C₁₂ to C₂₄ fatty alcohols, ethoxylated fattyacids or fatty amides; sodium, potassium, or ammonium salts of fattyacids, such as Na stearate and Na oleate; or combinations thereof. Theamount of emulsifier in the aqueous emulsion is preferably from about0.05 weight percent to about 10 weight percent, and more preferably fromabout 0.3 weight percent to about 3 weight percent, based on the totalweight of the monomers.

[0031] The macromonomer thus prepared is emulsion polymerized withethylenically unsaturated monomer to form a copolymer compositioncontaining graft copolymer particles. The polymerization is carried outby providing the macromonomer as water insoluble particles in amacromonomer aqueous emulsion and the ethylenically unsaturated monomerin a monomer composition. At least a portion of the macromonomer aqueousemulsion is combined with at least a portion of the monomer compositionto form a polymerization reaction mixture that is polymerized in thepresence of an initiator.

[0032] Although in no way intending to be bound in theory, it isbelieved that by providing the macromonomer in the form of waterinsoluble macromonomer particles in an aqueous emulsion, and theethylenically unsaturated monomer in a separate monomer composition,upon combination, the ethylenically unsaturated monomer diffuses intothe macromonomer particles where the polymerization occurs. Preferably,the diffusion of the ethylenically unsaturated monomer into themacromonomer particles is evidenced by swelling of the macromonomerparticles.

[0033] The macromonomer aqueous emulsion useful in the present inventionmay be formed in any manner known to those skilled in the art. Forexample, the macromonomer, produced by any known method, may be isolatedas a solid (e.g., spray dried) and emulsified in water. Also, forexample, the macromonomer, if prepared via an emulsion or aqueous basedpolymerization process, may be used as is, or diluted with water orconcentrated to a desired solids level.

[0034] In a preferred embodiment of the present invention, themacromonomer aqueous emulsion is formed from the emulsion polymerizationof an ethylenically unsaturated monomer in the presence of a transitionmetal chelate chain transfer agent as described previously herein. Thisembodiment is preferred for numerous reasons. For example, themacromonomer polymerization can be readily controlled to produce adesired particle size distribution (preferably narrow, e.g.,polydispersity less than 2). Also, for example, additional processingsteps, such as isolating the macromonomer as a solid, can be avoided,leading to better process economics. In addition, the macromonomer,macromonomer aqueous emulsion and the graft copolymer can be prepared byconsecutive steps in a single reactor which is desirable in a commercialmanufacturing facility.

[0035] The macromonomer aqueous emulsion useful in the present inventioncontains from about 20 weight percent to about 60 weight percent, andmore preferably from about 30 weight percent to about 50 weight percentof at least one water insoluble macromonomer, based on the total weightof macromonomer aqueous emulsion. The macromonomer aqueous emulsion mayalso contain mixtures of macromonomer. Preferably, the macromonomeraqueous emulsion contains less than about 5 weight percent and morepreferably less than about 1 weight percent of ethylenically unsaturatedmonomer, based on the total weight of macromonomer aqueous emulsion:.

[0036] The water insoluble macromonomer particles have a particle sizeto form graft copolymer of the desired particle size. For example, thefinal graft copolymer particles size is directly proportional to theinitial particle size of the macromonomer and the concentration ofethylenically unsaturated monomers in the polymerization reactionmixture, assuming all the particles participate equally in thepolymerization. Preferably, the macromonomer particles have a weightaverage particle size of from about 50 nm to about 500 nm, and morepreferably from about 80 nm to about 200 nm as measured by CapillaryHydrodynamic Fractionation technique using a Matec CHDF 2000 particlesize analyzer equipped with a HPLC type Ultra-violet detector.

[0037] The macromonomer aqueous emulsion may also include one or moreemulsifying agents. The type and amount of emulsifying agent ispreferably selected in a manner to produce the desired particle size.Suitable emulsifying agents include those previously disclosed for usein preparing the macromonomer by an emulsion polymerization process.Preferred emulsifying agents are anionic surfactants such as, forexample, sodium lauryl sulfate, sodium dodecylbenzene sulfonate,sulfated and ethoxylated derivatives of nonylphenols and fatty alcohols.The total level of emulsifying agent, based on the total weight ofmacromonomer is preferably from about 0.2 weight percent to about 5weight percent and more preferably from about 0.5 weight percent toabout 2 weight percent.

[0038] The monomer composition useful in the present invention containsat least one kind of ethylenically unsaturated monomer. The monomercomposition may contain all (i.e., 100%) monomer, or contain monomerdissolved or dispersed in an organic solvent and/or water. Preferably,the level of monomer in the monomer composition is from about 50 weightpercent to 100 weight percent, more preferably from about 60 weightpercent to about 90 weight percent, and most preferably from about 70weight percent to about 80 weight percent, based on the total weight ofthe monomer composition. Examples of organic solvents that may bepresent in the monomer composition include C₆ to C₁₄ alkanes. Theorganic solvent in the monomer composition will be no more than 30weight percent, and more preferably no more than 5 weight percent, basedon the total weight of the monomer composition.

[0039] In addition to water and/or organic solvent, the monomercomposition may also optionally contain monomers containing functionalgroups, such as, for example, monomers containing hydroxy, amido,aldehyde, ureido, polyether, glycidylalkyl, keto groups or combinationsthereof. These other monomers are generally present in the monomercomposition at a level of from about 0.5 weight percent to about 15weight percent, and more preferably from about 1 weight percent to about3 weight percent based on the total weight of the graft copolymer.Examples of functional monomers include ketofunctional monomers such asthe acetoacetoxy esters of hydroxyalkyl acrylates and methacrylates(e.g., acetoacetoxyethyl methacrylate) and keto-containing amides (e.g.,diacetone acrylamide); allyl alkyl methacrylates or acrylates;glycidylalkyl methacrylates or acrylates; or combinations thereof. Suchfunctional monomer can provide crosslinking if desired.

[0040] In a preferred embodiment, the monomers in the monomercomposition are preemulsified in water to form a monomer aqueousemulsion. Preferably, the monomer aqueous emulsion contains monomerdroplets having a droplet size from about 1 micron to about 100 microns,and more preferably from about 5 micron to about 50 microns. Anysuitable emulsifying agent may be used, for example those previouslydescribed, to emulsify the monomer to the desired monomer droplet size.Preferably, the level of emulsifying agent, if present, will be fromabout 0.2 weight percent to about 2 weight percent based on the totalweight of monomer in the monomer composition.

[0041] The ethylenically unsaturated monomer of the monomer compositionis preferably selected to provide the desired properties in theresulting copolymer composition. Suitable ethylenically unsaturatedmonomers include for example methacrylate esters, such as C₁ to C₁₈normal or branched alkyl esters of methacrylic acid, including methylmethacrylate, ethyl methacrylate, n-butyl methacrylate, 2-ethylhexylmethacrylate, lauryl methacrylate, stearyl methacrylate, isobornylmethacrylate; acrylate esters, such as C₁ to C₁₈ normal or branchedalkyl esters of acrylic acid, including methyl acrylate, ethyl acrylate,n-butyl acrylate and 2-ethylhexyl acrylate; styrene; substitutedstyrenes, such as methyl styrene, α-methyl styrene or t-butyl styrene;olefinically unsaturated nitriles, such as acrylonitrile ormethacrylonitrile; olefinically unsaturated halides, such as vinylchloride, vinylidene chloride or vinyl fluoride; vinyl esters of organicacids, such as vinyl acetate; N-vinyl compounds such as N-vinylpyrrolidone; acrylamide; methacrylamide; substituted acrylamides;substituted methacrylamides; hydroxyalkylmethacrylates such ashydroxyethylmethacrylate; hydroxyalkylacrylates; dienes such as1,3-butadiene and isoprene; vinyl ethers; or combinations thereof. Theethylenically unsaturated monomer can also be an acid containing monomeror a functional monomer, such as those previously described herein.Preferably, the ethylenically unsaturated monomer of the monomercomposition does not contain amino groups.

[0042] In a preferred embodiment, the monomer composition includes oneor more ethylenically unsaturated monomers selected from C₁ to C₁₈normal or branched alkyl esters of acrylic acid, including methylacrylate, ethyl acrylate, n-butyl acrylate and 2-ethylhexyl acrylate;styrene; substituted styrenes, such as methyl styrene, α-methyl styreneor t-butyl styrene; butadiene or combinations thereof.

[0043] As previously mentioned, the macromonomer aqueous emulsion andmonomer composition are combined to form a polymerization reactionmixture, and polymerized in the presence of a free radical initiator toform an aqueous copolymer composition. The term “polymerization reactionmixture,” as used herein, refers to the resulting mixture formed when atleast a portion of the macromonomer aqueous emulsion and at least aportion of the monomer composition are combined. The polymerizationreaction mixture may also contain initiator or any other additive usedduring the polymerization. Thus, the polymerization reaction mixture isa mixture that changes in composition as the macromonomer and monomer inthe monomer composition are reacted to form graft copolymer.

[0044] The macromonomer aqueous emulsion and monomer composition may becombined in various ways to carry out the polymerization. For example,the macromonomer aqueous emulsion and the monomer composition may becombined prior to the start of the polymerization reaction to form thepolymerization reaction mixture. Alternatively, the monomer compositioncould be gradually fed into the macromonomer aqueous emulsion, or themacromonomer aqueous emulsion could be gradually fed into the monomercomposition. It is also possible that only a portion of the macromonomeraqueous emulsion and/or monomer composition be combined prior to thestart of the polymerization with the remaining monomer compositionand/or macromonomer aqueous emulsion being fed during thepolymerization.

[0045] The initiator can also be added in various ways. For example, theinitiator may be added in “one shot” to the macromonomer aqueousemulsion, the monomer composition, or a mixture of the macromonomeraqueous emulsion and the monomer composition at the start of thepolymerization. Alternatively, all or a portion of the initiator can becofed as a separate feed stream, as part of the macromonomer aqueousemulsion, as part of the monomer composition, or any combination ofthese methods.

[0046] The preferred method of combining the macromonomer aqueousemulsion, the monomer composition, and initiator will depend on suchfactors as the desired graft copolymer composition. For example, thedistribution of the macromonomer as a graft along the backbone can beaffected by the concentrations of both the macromonomer and theethylenically unsaturated monomers at the time of the polymerization. Inthis regard, a batch process will afford high concentration of both themacromonomer and the ethylenically unsaturated monomers at the onset ofthe polymerization whereas a semi-continuous process will keep theethylenically unsaturated monomer concentration low during thepolymerization. Thus, through the method in which the macromonomeraqueous emulsion and monomer composition are combined, it is possible tocontrol, for example, the number of macromonomer grafts per polymerchain, the distribution of graft in each chain, and the length of thepolymer backbone.

[0047] Initiators useful in polymerizing the macromonomer andethylenically unsaturated monomer include any suitable initiator foremulsion polymerizations known to those skilled in the art. Theselection of the initiator will depend on such factors as theinitiator's solubility in one or more of the reaction components (e.g.monomer, macromonomer, water); and half life at the desiredpolymerization temperature (preferably a half life within the range offrom about 30 minutes to about 10 hours). Suitable initiators includethose previously described herein in connection with forming themacromonomer, such as azo compounds such as 4,4′-azobis(4-cyanovalericacid), peroxides such as t-butyl hydroperoxide; sodium, potassium, orammonium persulfate; redox initiator systems such as, for example,persulphate or peroxide in combination with a reducing agent such assodium metabisulfite, sodium bisulfite, sodium formaldehyde sulfoxylate,isoascorbic acid; or combinations thereof. Metal promoters, such asiron; and buffers, such as sodium bicarbonate, may also be used incombination with the initiator. Additionally, Controlled Free RadicalPolymerization (CFRP) methods such as Atom Transfer RadicalPolymerization; or Nitroxide Mediated Radical Polymerization may beused. Preferred initiators include azo compounds such as4,4′-azobis(4-cyanovaleric acid).

[0048] The amount of initiator used will depend on such factors as thecopolymer desired and the initiator selected. Preferably, from about 0.1weight percent to about 1 weight percent initiator is used, based on thetotal weight of monomer and macromonomer.

[0049] The polymerization temperature will depend on the type ofinitiator chosen and desired polymerization rates. Preferably, however,the macromonomer and ethylenically unsaturated monomer are polymerizedat a temperature of from about room temperature to about 1 50° C., andmore preferably from about 40° C. to about 95° C.

[0050] The amount of macromonomer aqueous emulsion and monomercomposition added to form the polymerization reaction mixture willdepend on such factors as the concentrations of macromonomer andethylenically unsaturated monomer in the macromonomer aqueous emulsionand monomer composition, respectively, and the desired copolymercomposition. Preferably, the macromonomer aqueous emulsion and monomercomposition are added in amounts to provide a copolymer containing aspolymerized units of from about 2 weight percent to about 90 weightpercent, more preferably from about 5 weight percent to about 50 weightpercent, and most preferably from about 5 weight percent to about 35weight percent macromonomer, and from about 10 weight percent to about98 weight percent, more preferably from about 50 weight percent to about95 weight percent and most preferably from about 65 weight percent toabout 95 weight percent ethylenically unsaturated monomer.

[0051] One skilled in the art will recognize that other components usedin conventional emulsion polymerizations may optionally be used in themethod of the present invention. For example, to reduce the molecularweight of the resulting graft copolymer, the polymerization mayoptionally be conducted in the presence of one or more chain transferagents, such as n-dodecyl mercaptan, thiophenol; halogen compounds suchas bromotrichloromethane; or combinations thereof. Also, additionalinitiator and/or catalyst may be added to the polymerization reactionmixture at the completion of the polymerization reaction to reduce anyresidual monomer, (e.g., chasing agents). Suitable initiators orcatalysts include those initiators previously described herein. Inaddition, the chain transfer capacity of a macromonomer throughaddition-fragmentation can be utilized in part to reduce molecularweight through appropriate design of monomer compositions andpolymerization conditions. See e.g., E. Rizzardo, et. al., Prog. PacificPolym. Sci., 1991, 1, 77-88; G. Moad, et. al., WO 96/15157.

[0052] Preferably, the process of the present invention does not requireneutralization of the monomer, or resulting aqueous copolymercomposition. These components preferably remain in unneutralized form(e.g., no neutralization with a base if acid functional groups arepresent).

[0053] The resulting aqueous copolymer composition formed bypolymerization of the macromonomer and the ethylenically unsaturatedmonomer in the monomer composition preferably has a solids level of fromabout 30 weight percent to about 65 weight percent and more preferablyfrom about 40 weight percent to about 60 weight percent. The aqueouscopolymer composition preferably contains copolymer particles that arewater insoluble and have a particle size of from about 60 nm to about500 nm, and more preferably from about 80 nm to about 200 nm.

[0054] The graft copolymer formed preferably has a backbone containing,as polymerized units, the ethylenically unsaturated monomer from themonomer composition, and one or more side chains, pendent from thebackbone, containing the macromonomer. Preferably, each side chain isformed from one macromonomer grafted to the backbone. The degree ofpolymerization of the macromonomer side chains is preferably in therange of from about 10 to about 1000, and more preferably in the rangeof from about 20 to about 200, where the degree of polymerization isexpressed as the number of polymerized units of ethylenicallyunsaturated monomer used to form the macromonomer. The total weightaverage molecular weight of the graft copolymer is preferably in therange of from about 50,000 to about 2,000,000, and more preferably fromabout 100,000 to about 1,000,000. Weight average molecular weights asused herein can be determined by size exclusion chromatography.

[0055] The copolymer particles of the aqueous copolymer composition canbe isolated, for example, by spray drying or coagulation. However, it ispreferable to use the copolymer aqueous composition as is.

[0056] In a preferred embodiment of the present invention, thepolymerization is conducted in two stages. In the first stage, themacromonomer is formed in an aqueous emulsion polymerization process,and in the second stage the macromonomer is polymerized with theethylenically unsaturated monomer in an emulsion. For efficiency,preferably these two stages are conducted in a single vessel. Forexample, in the first stage, the macromonomer aqueous emulsion may beformed by polymerizing in an aqueous emulsion at least one firstethylenically unsaturated monomer to form water insoluble macromonomerparticles. This first stage polymerization is preferably conducted usinga transition metal chelate chain transfer agent as previously describedherein. After forming the macromonomer aqueous emulsion, a secondemulsion polymerization is preferably performed in the same vessel topolymerize the macromonomer with at least one second ethylenicallyunsaturated monomer. This second stage may be conducted for example bydirectly adding (e.g., all at once or by a gradual feed) the monomercomposition and initiator to the macromonomer aqueous emulsion. One mainadvantage of this embodiment is that the macromonomer does not have tobe isolated, and the second polymerization can take place simply byadding the monomer composition and initiator to the macromonomer aqueousemulsion.

[0057] In another preferred embodiment of the present invention, thepolymerization of the macromonomer and ethylenically unsaturated monomeris at least partially performed in the presence of an acid containingmonomer, acid containing macromonomer, or combinations thereof. The acidcontaining monomer or acid containing macromonomer may be added in anymanner to the polymerization reaction mixture. Preferably, the acidcontaining monomer or acid containing macromonomer is present in themonomer composition. The acid containing monomer or acid containingmacromonomer may also be added as a separate stream to thepolymerization reaction mixture.

[0058] The amount of acid containing monomer or acid containingmacromonomer added to the polymerization reaction mixture is preferablyfrom about 0.2 weight percent to about 10 weight percent, morepreferably from about 0.5 weight percent to about 5 weight percent, andmost preferably from about 1 weight percent to about 2 weight percent,based on the total weight of monomer and macromonomer added to thepolymerization reaction mixture.

[0059] Acid containing monomers which may be used in this embodimentinclude ethylenically unsaturated monomers bearing acid functional oracid forming groups such as those previously described herein. The acidcontaining macromonomer useful in this embodiment is any low molecularweight polymer having at least one terminal ethylenically unsaturatedgroup that is capable of being polymerized in a free radicalpolymerization process, and that is formed from at least one kind ofacid containing monomer. Preferably, the amount of acid containingmonomer in the acid containing macromonomer is from about 50 weightpercent to 100 weight percent, more preferably from about 90 weightpercent to 100 weight percent, and most preferably from about 95 weightpercent to 100 weight percent.

[0060] The acid containing macromonomer may be prepared according to anytechnique known to those skilled in the art such as those previouslydescribed herein. In a preferred embodiment of the present invention,the acid containing macromonomer is prepared by a solutionpolymerization process using a free radical initiator and transitionmetal chelate complex. An example of such a process is disclosed in forexample U.S. Pat. No. 5,721,330, which is incorporated by reference inits entirety. Preferred acid containing monomers used to form the acidcontaining macromonomer are α-methyl vinyl monomers such as methacrylicacid.

[0061] In another preferred embodiment of the present invention, amacromolecular organic compound having a hydrophobic cavity is presentin the polymerization medium used to form the macromonomer and/oraqueous copolymer composition. Preferably, the macromolecular organiccompound is used when copolymerizing ethylenically unsaturated monomerswith very low water solubility such as lauryl or stearyl acrylatesand/or methacrylates. By “low water solubility” it is meant a watersolubility at 25° C. to 50° C. of no greater than 50 millimoles/liter.For example, the macromolecular organic compound may be added to themonomer composition, the macromonomer aqueous emulsion, or thepolymerization reaction mixture used to form the aqueous copolymercomposition. Also, for example the macromolecular organic compound maybe added to an aqueous emulsion of ethylenically unsaturated monomerused to form the macromonomer. Suitable techniques for using amacromolecular organic compound having a hydrophobic cavity aredisclosed in, for example, U.S. Pat. No. 5,521,266, the disclosure ofwhich is hereby incorporated by reference in its entirety.

[0062] Preferably, the macromolecular organic compound having ahydrophobic cavity is added to the polymerization reaction mixture toprovide a molar ratio of macromolecular organic compound to low watersolubility monomer or macromonomer of from about 5:1 to about 1:5000 andmore preferably from about 1:1 to about 1:500.

[0063] Macromolecular organic compounds having a hydrophobic cavityuseful in the present invention include for example cyclodextrin orcyclodextrin derivatives; cyclic oligosaccharides having a hydrophobiccavity such as cycloinulohexose, cycloinuloheptose, or cycloinuloctose;calyxarenes; cavitands; or combinations thereof. Preferably, themacromolecular organic compound is β-cyclodextrin, more preferablymethyl-β-cyclodextrin.

[0064] Monomers having low water solubility include for example primaryalkenes; styrene and alkylsubstituted styrene; α-methyl styrene;vinyltoluene; vinyl esters of C₄ to C₃₀ carboxylic acids, such as vinyl2-ethylhexanoate, vinyl neodecanoate; vinyl chloride; vinylidenechloride; N-alkyl substituted (meth)acrylamide such as octyl acrylamideand maleic acid amide; vinyl alkyl or aryl ethers with (C₃-C₃₀) alkylgroups such as stearyl vinyl ether; (C₁-C₃₀) alkyl esters of(meth)acrylic acid, such as methyl methacrylate, ethyl (meth)acrylate,butyl (meth)acrylate, 2-ethylhexyl (meth)acrylate, benzyl(meth)acrylate, lauryl (meth)acrylate, oleyl (meth)acrylate, palmityl(meth)acrylate, stearyl (meth)acrylate; unsaturated vinyl esters of(meth)acrylic acid such as those derived from fatty acids and fattyalcohols; multifunctional monomers such as pentaerythritol triacrylate;monomers derived from cholesterol or combinations thereof.

[0065] In another aspect of the present invention an aqueous copolymercomposition is provided that is preferably produced by the method of thepresent invention as previously described herein. The aqueous copolymercomposition contains water insoluble particles of graft copolymer thatare preferably comb copolymer particles. The comb copolymer particlespreferably have a weight average particle size of from about 50 nm toabout 500 nm, and more preferably from about 80 nm to about 200 nm.

[0066] Preferably, the particles of graft copolymer contain from about 2weight percent to about 90 weight percent, and more preferably fromabout 5 weight percent to about 50 weight percent polymerized units of amacromonomer, based on the total weight of the copolymer, where themacromonomer preferably has a composition as previously described hereinfor the water insoluble macromonomer present in the macromonomer aqueousemulsion. The graft copolymer particles also preferably contain fromabout 10 weight percent to about 98 weight percent, and more preferablyfrom about 50 weight percent to about 95 weight percent polymerizedunits of at least one ethylenically unsaturated monomer, based on thetotal weight of the copolymer. The ethylenically unsaturated monomer maybe any ethylenically unsaturated monomer that provides desirableproperties in the copolymer particles, such as those useful in themonomer composition as previously described herein.

[0067] Preferably, the backbone of the graft copolymer is linear.Compositionally, the backbone of the copolymer preferably containspolymerized units of the ethylenically unsaturated monomer derived fromthe monomer composition. Preferably, the backbone contains less than 20mole percent, and more preferably less than 10 mole percent ofpolymerized macromonomer derived from the macromonomer aqueous emulsionbased on the total moles of the copolymer.

[0068] The side chains of the graft copolymer preferably containpolymerized units of the macromonomer. In a preferred embodiment of thepresent invention, each side chain comprises one macromonomer.Additionally, the side chains contain less than 5 weight percent andmore preferably less than 1 weight percent of the polymerizedethylenically unsaturated monomer derived from the monomer composition,based on the total weight of the side chains.

[0069] Preferably, the overall weight average molecular weight of thegraft copolymer is from about 50,000 to about 2,000,000, and morepreferably from about 100,000 to about 1,000,000.

[0070] In a preferred embodiment of the present invention, the waterinsoluble copolymer particles further contain from about 0.2 weightpercent to about 10 weight percent, more preferably from about 0.5weight percent to about 5 weight percent, and most preferably from about1 weight percent to about 2 weight percent of an acid containingmacromonomer, based on the total weight of the graft copolymer. The acidcontaining macromonomer preferably has a composition as previouslydescribed herein.

[0071] Although in no way intending to be bound by theory, it isbelieved that the acid containing macromonomer is attached to thesurface of the water insoluble graft copolymer particles and providesstability. By “attached,” as used herein, it is believed that the acidcontaining macromonomer is bound in some manner (e.g., covalent,hydrogen bonding, ionic) to a polymer chain in the particle. Preferably,the acid containing macromonomer is covalently bound to a polymer chainin the particle. It has been found that the acid containing macromonomerprovides stability to the particles such that the aqueous copolymercomposition produced exhibits unexpected improved shear stability;freeze thaw stability; and stability to additives in formulations, aswell as reduction of coagulums during the polymerization. Althoughimproved stability can be achieved using acid containing monomer, thesebenefits are most dramatic when an acid containing macromonomer is used.

[0072] The aqueous copolymer composition in addition to the copolymerparticles preferably contains less than about 10 weight percent, andmore preferably less than about 1 weight percent of organic solvent. Ina most preferred embodiment, the aqueous copolymer composition containsno organic solvent.

[0073] An advantage of using the method of the present invention toprepare the aqueous copolymer composition is that the resultingcopolymer composition contains low levels of homopolymer, such as forexample homopolymer of ethylenically unsaturated monomer derived fromthe monomer composition or homopolymer of macromonomer derived from themacromonomer aqueous emulsion. Preferably the aqueous copolymercomposition contains less than about 30 weight percent and morepreferably less than about 20 weight percent of homopolymer ofmacromonomer, based on the total weight of the graft copolymer.Preferably also the aqueous copolymer composition contains less thanabout 30 weight percent and more preferably less than about 20 weightpercent of homopolymer of ethylenically unsaturated monomer.

[0074] The aqueous copolymer compositions produced by the method of thepresent invention are useful in a variety of applications. For example,the aqueous copolymer compositions may be used in architectural andindustrial coatings including paints, wood coatings, or inks; papercoatings; textile and nonwoven binders and finishes; adhesives; mastics;floor polishes; leather coatings; plastics; plastic additives; petroleumadditives; thermoplastic elastomers or combinations thereof.

EXAMPLES

[0075] Some embodiments of the invention will now be described in detailin the following Examples. The following abbreviations shown in Table 1are used in the examples: TABLE 1 Abbreviations Abbreviation A-16-22Polystep A-16-22, anionic surfactant, supplied as 22% solids by StepanCompany, located in Northfield, Illinois. BA Butyl acrylate BD ButadieneBMA Butyl methacrylate CoBF Co(II)-(2,3-dioxyiminobutane-BF₂)₂ CVA4,4-azobis(4-cyanovaleric acid) Fe 0.15% Ferrous sulfate in water DBSDodecyl benzene sulfonate GC Gas chromatograph SEC Size exclusionchromatography HPLC High performance liquid chromatography Init.Initiator IR Infrared spectroscopy LCCC Liquid chromatography undercritical conditions MAA Methacrylic acid MMA Methyl methacrylate MnNumber average molecular weight NaMBS Sodium metabisulfite NaPS Sodiumpersulfate nDDM Dodecyl mercaptan OT-100 Aerosol OT-100, anionicsurfactant, supplied as 100% active by Cytec Industries Inc., located inMorristown, New Jersey. PMAA-MM Poly-methacrylic acid macromonomer PMMAMethyl methacrylate homopolymer PMMA-MM Poly-methyl methacrylatemacromonomer Poly-(BA-g-BMA) Graft copolymer of BA with BMA side chainsPoly-(BA-g-MMA) Graft copolymer of BA with MMA side chainsPoly-(BD-g-MMA) Graft copolymer of BD with MMA side chains Wako VA-0442,2′-azobis[2-(2-imidazolin2-2yl)propane] dihydrochloride

[0076] In the Examples, monomer conversion was determined by GC analysisof unreacted monomer using standard methods. Weight percent solids forthe macromonomer and copolymer compositions were determined bygravimetric analysis. Particle size of the macromonomer and copolymercompositions were obtained using a Matec CHDF 2000 particle sizeanalyzer equipped with a HPLC type Ultra-violet detector.

[0077] Except where noted differently, macromonomer was measured fornumber average molecular weight by SEC using a polystyrene standard fromPolymer Laboratories (PS-I) having a peak average molecular weightranging from 580 to 7,500,000 with narrow molecular weight distribution.Conversions from polystyrene to PMMA were made using Mark-Houwinkconstants. Copolymer compositions were evaluated for number averagemolecular weight and weight average molecular weight using SEC asdescribed above.

Comparative Example 1.0

[0078] Low molecular weight MMA polymer was prepared by an aqueousemulsion polymerization process using a conventional chain transferagent. The polymerization was conducted in a 2-liter, four neck roundbottom reaction flask equipped with a mechanical stirrer, temperaturecontrol device, condenser, monomer feed line and a nitrogen inletaccording to the following procedure. To the reaction flask were added483.7 grams of deionized water, 2.0 grams of A-16-22, and 1.55 grams ofan aqueous solution containing 52 wt % methyl-β-cyclodextrin to form asurfactant solution. A monomer emulsion containing 125 g of deionizedwater, 3 g of A-16-22, 305 g of MMA and 5 g of nDDM was preparedseparately. Additionally, an initiator solution was prepared bydissolving 1.56 g of NaBS in 72.3 g of deionized water. The surfactantsolution was heated to 80° C. after which 60% of the total initiatorsolution was added to the reaction flask. The monomer emulsion and theremaining initiator solution were then fed over a period of 60 minutes.At the end of the feed period, the reaction mixture was maintained at80° C. for an additional 30 minutes, followed by cooling and filtering.The resulting low molecular weight MMA emulsion contained 31.0 wt %solids. The MMA polymer had a number average molecular weight (Mn) of21700.

Examples 1.1 to 1.8 Preparation of PMMA-MM by Emulsion Polymerization

[0079] MMA macromonomer (PMMA-MM) was prepared by emulsionpolymerization processes in Examples 1.1 to 1.8 using the same equipmentdescribed in Comparative Example 1.0. The specific amounts of water,surfactant, MMA, chain transfer agent (CTA), and initiator used inExamples 1.1 to 1.8 are shown in Table 2. These ingredients were addedaccording to the following procedure. In a different flask from thereaction flask, a monomer solution was prepared by dissolving the chaintransfer agent in MMA under a nitrogen purge. Deionized water andsurfactant (OT-100) were introduced into the reaction flask at roomtemperature to form a water surfactant solution. The water surfactantsolution was mixed and heated to 80° C. with stirring under a nitrogenpurge. Upon reaching a temperature of 80° C., and upon completedissolution of the surfactant, the initiator (CVA) was added to thewater surfactant solution with stirring for 1 minute to permit theinitiator to dissolve. After dissolution of the initiator, 20 percent byweight of the monomer solution was added to the reaction flask withstirring. Following this initial charge, the remaining monomer solutionwas fed over a period of 1 to 2 hours, with stirring, to form a reactionmixture. At the end of the feed period, the reaction mixture wasmaintained at 80° C. for an additional 1 to 3 hours. The reactionmixture was then cooled to room temperature and passed through a filtercloth to remove any coagulum.

[0080] Generally, the resulting macromonomer emulsion contained lessthan 5 weight percent coagulum based on the total weight ofmacromonomer, and the conversion of monomer was over 99 weight percent,based on the total weight of monomer added. The Mn, weight percentsolids and particle size for each macromonomer are reported in Table 2.TABLE 2 Preparation of PMMA-MM Part. Surfactant MMA CTA Initiator SizeWt % Example H₂O (g) (g)⁽³⁾ (g) ppm⁽¹⁾ g⁽²⁾ (nm) Mn Solids 1.1 720 3.6324 40 3.6 165 2430 32.0 1.2 720 3.6 324 8.7 3.6 126 12612 31.0 1.3 7203.6 324 10.9 3.6 158 9656 31.0 1.4 720 3.6 324 80.6 3.6 231 1386 30.31.5 720 3.6 324 21.8 3.6 201 4416 29.1 1.6 720 3.6 324 10.7 3.6 169 793130.5 1.7 720 3.6 360 11.9 3.6 155 10185 32.0 1.8 1440 7.2 720 15.2 7.2167 7237 32.0

Example 2 Preparation of PMAA-MM By Solution Polymerization

[0081] An MAA macromonomer (PMAA-MM) was prepared by an aqueous solutionpolymerization process in a 2-liter baffled flange flask equipped with amechanical stirrer, condenser, temperature control device, initiatorfeed lines and a nitrogen inlet. The apparatus was purged with nitrogenfor 30 minutes after 0.018 g of CoBF was added. Deionized water, 1080 g,was charged to the flask and heated to 55° C. under a nitrogen purge. Amonomer mixture containing 510 ml of MAA and 0.01 g of CoBF was preparedseparately under nitrogen. When the deionized water reached atemperature of 55° C., 1.94 g of initiator (Wako VA-044) was added tothe reaction flask. Following the addition of the initiator, the monomermixture was added over a period of 60 minutes to the reaction flask withstirring. The temperature was then held at 55° C. for 2 hours followingcompletion of the monomer mixture feed. Upon cooling the reaction flaskto room temperature, the MAA-MM (Example 2.1) was isolated as driedpolymer by rotary evaporation. The number average molecular weight (Mn)of the MAA-MM was determined by proton nuclear magnetic resonance to be4030 based on the integration of the vinyl end group with respect to themethyl and methylene groups of the polymer chain.

Example 3 Preparation of Poly-(BA-g-MMA) Graft Copolymers by BatchEmulsion Polymerization Process

[0082] Comparative Example 3.0C and Examples 3.1 to 3.15 graftcopolymers were prepared by a batch emulsion polymerization process in a1-liter, four neck round bottom reaction flask equipped with amechanical stirrer, condenser, temperature control device, initiatorfeed lines and a nitrogen inlet. The specific amounts of PMMA-MM (asemulsion), water, surfactant, acid containing monomer (marked “acid”0 inTable 3), BA, initiator, and buffer used are shown in Table 3. Theseingredients were added according to the following procedure. Deionizedwater (H₂O #1 in Table 3) and PMMA-MM emulsion obtained from the exampleindicated in Table 3 (sub-column marked “Ex” under the “PMMA-MM” column)were introduced into the reaction flask at room temperature. A monomeremulsion of deionized water (H₂O #2 in Table 3), surfactant, acidcontaining monomer, and BA was prepared. The monomer emulsion in Example3.13 additionally contained 0.13 g of NDDM. The monomer emulsion wasintroduced into the reaction flask at room temperature with stirring toform a reaction mixture. After stirring for 20 minutes, the reactionmixture was heated to the reaction temperature indicated in Table 3.

[0083] Once the reaction temperature was reached, an initiator andoptionally a buffer were introduced into the reaction flask withstirring according to the following procedures. For examples 3.1C; 3.2;3.3 and 3.4 to 3.8, both the buffer and initiator listed in Table 3 wereadded as a single shot to the reaction flask. For examples 3.9 to 3.12and 3.16, 20% by weight of the initiator solution was added in one shotto the reaction flask, with the remainder being fed over 1 to 2 hours.For the examples prepared with a redox initiator (3.13 to 3.15), onethird of the NaPS and NaMBS were added in one shot to the reactionflask, with the remainder fed over 1 to 2 hours. Also, for the redoxinitiator system, all of the Fe and Na₂CO₃ were added to the reactionflask at the beginning of the NaPS and NaMBS feeds. After the initiatorand buffer were added, the reaction mixture was maintained at thereaction temperature for a period of 1 to 2 hours. The resultingcopolymer composition was analyzed for conversion and other propertiesas described in Example 10. The conversion of BA, as determined bystandard GC methods, was greater than 99 weight percent based on thetotal weight of BA charged. TABLE 3 Preparation of Poly-(BA-g-MMA) GraftCopolymers Prepared by Batch Process PMMA- MM H₂O H₂O Amt. #1 #2Surf.⁽²⁾ BA Temp. Init. Buffer⁽⁹⁾ Acid Example Ex (g) (g) (g) (g) (g) (°C.) (g) (g) (g) 3.1 C⁽⁸⁾ 1.0 146.7 22 25 2.2 82.6 90 0.09⁽⁵⁾ 0.1 1.96⁽⁷⁾3.2 1.4 100 14 20.8 0.49 55.7 70 0.63⁽³⁾ 0 0 3.3 1.3 97 17 20.8 0.4955.7 70 0.63⁽³⁾ 0 0 3.4 1.1 50.8 0 19 1.1 47.8 80 0.07⁽⁵⁾ 0.05 0.98⁽⁷⁾3.5 1.5 52 0 19 1.1 47.8 80 0.07⁽⁵⁾ 0.05 0.98⁽⁷⁾ 3.6 1.6 53.3 0 20.3 1.147.8 80 0.07⁽⁵⁾ 0.04 0.98⁽⁷⁾ 3.7 1.3 52.4 0 19 1.1 47.8 80 0.07⁽⁵⁾ 0.050.98⁽⁷⁾ 3.8 1.2 52 0 19 1.1 47.8 80 0.07⁽⁵⁾ 0.05 0.98⁽⁷⁾ 3.9 1.3 216 5946.8 1.1 123.8 80 1.05⁽⁵⁾ 0 2.3⁽⁶⁾ 3.10 1.3 84 77 39 0.91 103 80 0.07⁽⁵⁾0 1.3⁽⁶⁾ 3.11 1.3 42 42 102 1.02 115 80 0.07⁽⁵⁾ 0 1.3⁽⁶⁾ 3.12 1.3 21 11246.3 1.08 122.5 80 0.07⁽⁵⁾ 0 1.3⁽⁶⁾ 3.13 1.8 71 0 20 1.1 41.3⁽¹⁾ 90Redox⁽⁴⁾ 0.05 0.98⁽⁷⁾ 3.14 1.8 71.1 0 14 1.1 41.3 70 Redox⁽⁴⁾ 0.050.98⁽⁷⁾ 3.15 1.8 71.1 0 14 1.1 41.3 95 Redox⁽⁴⁾ 0.05 0.98⁽⁷⁾ 3.16 1.372.8 17 15.6 0.37 41.3 80 0.35⁽⁵⁾ 0 0.75⁽⁶⁾

Example 4 Preparation of Poly-(BA-g-MMA) by Semi-continuous Process

[0084] In Examples 4.1 to 4.5, graft copolymers were prepared by asemi-continuous emulsion polymerization process in a 1-liter roundbottom flask with four neck equipped with a mechanical stirrer,temperature control device, initiator feed lines and a nitrogen inlet.The specific amounts of PMMA-MM (as emulsion), water, surfactant, BA,acid containing monomer, and initiator used in Examples 4.1 to 4.4 areshown in Table 4. These ingredients were added according to thefollowing procedure. A monomer emulsion of deionized water (H₂O #2 inTable 4), surfactant, and BA was prepared in a separate flask. Themonomer emulsion in Example 4.2 additionally contained 0.13 g of nDDM.Deionized water (H₂O #1 in Table 4), acid containing monomer, andPMMA-MM obtained from the example indicated in Table 4 (subcolumn marked“Ex” under the “PMMA-MM” column) were introduced into the reaction flaskat room temperature to form a reaction mixture. The reaction mixture washeated to the reaction temperature indicated in Table 4 while stirringunder a nitrogen purge. Upon reaching the reaction temperature, aninitiator and buffer (if desired) were introduced into the reactionflask with stirring according to the following procedures. For examples4.1 to 4.3 (prepared with a redox initiator), one third of the NaPS andNaMBS, and all of the Fe and Na₂CO₃ were added in one shot to thereaction flask. The remaining NaPS and NaMBS was then cofed with themonomer emulsion over a 90 minute period. In Example 4.4, one third ofthe NaPS, and all of the Na₂CO₃ were added in one shot to the reactionflask, followed by cofeeding the monomer emulsion with the remainingNaPS over a 90 minute period. Upon completion of the feeds, the reactionmixture was maintained at the reaction temperature for a period of 1 to2 hours. The resulting copolymer composition was analyzed for conversionand other properties as described in Example 10. The conversion of BA,determined by standard GC methods, was greater than 99 weight percentbased on the total weight of BA charged. TABLE 4 Preparation ofPoly-(BA-g-MMA) Prepared by Semi-Continuous Process PMMA- MM H₂O H₂OAmt. #1 #2 Surf.⁽²⁾ BA Temp. Init. Buffer⁽⁵⁾ Acid Example Ex (g) (g) (g)(g) (g) (° C.) (g) (g) (g)⁽⁶⁾ 4.1 1.7 69.4 12 23 1.1 41.3 90 Redox⁽³⁾0.05 0.98 4.2 1.8 71 10.0 10 1.1 41.3⁽¹⁾ 90 Redox⁽³⁾ 0.11 0.98 4.3 1.871 10.0 10 1.1 41.3 90 Redox⁽³⁾ 0.11 0.98 4.4 1.8 71 10.3 18 1.1 41.3 900.16⁽⁴⁾ 0.11 0.98

Example 5 Preparation of Poly-(BD-g-MMA) graft copolymers

[0085] A graft copolymer having a backbone of BD and side chains of MMAwas prepared in accordance with the method of the present invention. Thegraft copolymer was prepared in two stages. In the first stage, PMMA-MMwas prepared in accordance with the procedure used in Example 1, exceptthat the following amounts of ingredients shown in Table 5a were used toreplace the corresponding ingredients in Table 2: TABLE 5a Ingredientsused in Preparation of BMA Macromonomer Ingredient Amount Charged H₂O2380 g Surfactant (A-16-22) 55 g MMA 1197 g CoBF 10.9 ppm⁽¹⁾ Initiator(CVA) 12.6 g

[0086] The resulting PMMA-MM had an Mn of 10,200.

[0087] In the second stage, a graft poly-(BD-g-MMA) was prepared in asteel pressure reactor equipped with a mechanical stirrer, temperaturecontrol device, and feed lines. Ingredients A through D, shown in Table5b, were charged to the reactor at room temperature. The reactor wasthen sealed and vacuum was applied, with stirring, to reduce the reactorpressure to 15 inches of Hg. Butadiene (E) in Table 5b was quicklypumped into the reactor and stirred for 10 minutes. Following stirringthe reaction mixture was heated to 60° C. for 30 minutes. After thereactor temperature stabilized to 60° C., ingredients F, G, and H inTable 5b were gradually pumped into the reactor over a period of 7hours. Following completion of the feeds, the reaction mixture was heldfor 60 minutes at 60° C. TABLE 5b Ingredients used in Preparation ofPoly- (BD-g-MMA) Graft Copolymer Ingredient Amount Charged A H₂O #16049.4 g B Acetic acid   4.3 g C PMMA-MM (as emulsion) 1389.71 g (Example 5a) D H₂O #2 (use for rinsing)   250 g E BD  877.5 g F t-butylperoxide (2% solution) 197.44 g G SFS⁽¹⁾ (1% solution) 263.25 g HAerosol-OT (75% solution)  3.51 g # scanning calorimetry showed twophase transitions at −79.8° and 110.4° C., respectively. The graftcopolymer composition had a solids content of 15 wt % and weight averageparticle size of 107 nm.

Example 6 Preparation of Poly-(BA-g-BMA) Graft Copolymer

[0088] A graft copolymer having a backbone of BA and side chains of BMAwas prepared in accordance with the method of the present invention. Thegraft copolymer was prepared in two stages. In the first stage, butylmethacrylate macromonomer was prepared in accordance with the procedureused in Example 1, except that the following amounts of ingredientsshown in Table 6a were used to replace the corresponding ingredients inTable 2: TABLE 6a Ingredients used in Preparation of BMA MacromonomerIngredient Amount Charged H₂O 720 g Surfactant (Aerosol OT-100) 3.6 gBMA 324 g CoBF 10.9 ppm⁽¹⁾ Initiator (CVA) 3.6 g

[0089] The resulting BMA macromonomer had an Mn of 8900.

[0090] In the second stage, a graft poly-(BA-g-BMA) was prepared usingthe procedure described in Example 3, except that the following amountsof ingredients shown in Table 6b were used to replace the correspondingingredients in Table 3, and a reaction temperature of 85° C. was used.TABLE 6b Ingredients used in Preparation of Poly- (BA-g-BMA) GraftCopolymer Ingredient Amount Charged PBMA-MM (as emulsion) 84.1 g(Example 6a) H₂O #2   15 g Surfactant⁽²⁾  1.1 g BA 41.3 g InitiatorRedox⁽¹⁾ Acid (PMAA-MM) 0.98 g (Example 2.1)

[0091] The graft copolymer formed contained 63.5 weight percent BA, 35weight percent of PBMA-MM and 1.5 weight percent of PMAA-MM.

Example 7 Preparation of Poly-(Styrene-g-MMA) Graft Copolymer

[0092] A graft copolymer having a backbone of styrene and side chains ofPMMA-MM was prepared in accordance with the method of the presentinvention. The graft copolymer was prepared in two stages. MacromonomerPMMA-MM (obtained from Example 1.8) was used in the synthesis of thegraft Poly-(Styrene-g-MMA). The graft Poly-(Styrene-g-MMA) was preparedusing the procedure described in Example 3 except that the followingamounts of ingredients shown in Table 7 were used to replace thecorresponding ingredients in Table 3, and a reaction temperature of 85°C. was used. TABLE 7 Ingredients used in Preparation of Poly-(Styrene-g-MMA) Graft Copolymer Ingredient Amount Charged PMMA-MM (asemulsion) 84.1 g (Example 1.8) H₂O #2   15 g Surfactant⁽²⁾  1.1 gStyrene 41.3 g Initiator Redox⁽¹⁾ Acid (pMAA-MM) 0.98 g (Example 2.1)

[0093] The graft copolymer formed contained 63.5 weight percent styrene,35 weight percent of PMMA-MM and 1.5 weight percent of PMAA-MM.

Example 8 Preparation of Poly-(BA-g-MMA) by a Single Vessel SynthesisProcedure

[0094] A graft copolymer having a backbone of BA and side chains of MMAwas prepared in accordance with the method of the present invention in asingle vessel in two aqueous emulsion polymerization stages. In thefirst stage, PMMA-MM was prepared and in the second stage the PMMA-MMwas copolymerized with BA.

[0095] The PMMA-MM was prepared in a four neck, 5-liter round bottomreaction flask equipped with a mechanical stirrer, temperature controldevice, condenser, monomer feed line and a nitrogen inlet. The reactionflask was charged with 680 g of deionized water and 15.7 g of A-16-22 toform a water surfactant solution. The water surfactant solution washeated with stirring to 80° C. under a nitrogen purge. At 80° C., 3.6 gof 4,4-azobis(4-cyanovaleric acid) was added with stirring to thereaction flask. Two minutes later, 18 g of MMA was added to the reactionflask with stirring. A monomer mixture containing 342 g of MMA and 0.02g of CoBF was prepared separately and degassed by bubbling nitrogen inthe monomer mixture for 20 minutes. A 20% by weight portion of themonomer mixture was added to the reaction flask 10 minutes after addingthe 18 g of MMA. The remainder of the monomer mixture was fed over 120minutes with stirring while maintaining the temperature at 80° C. At theend of the monomer mixture feed, the temperature of the reaction mixturein the flask was kept at 80° C. for 60 minutes and then cooled to 40° C.The resulting macromonomer aqueous emulsion was reacted in the samevessel in a second stage as described below.

[0096] In the second stage, a monomer emulsion containing 226 g ofdeionized water, 16.52 g of an ethoxylated C₆ to C₁₈ alkyl ether sulfate(30 wt % active) having from 1 to 40 ethylene oxide groups per molecule(30% active in water), 658 g of butyl acrylate was prepared. Inaddition, 10.2 g of PMAA-MM, in 75.4 g of water was prepared separately.The monomer emulsion and the PMAA-MM solution were added to the reactionflask at 40° C., and the resulting reaction mixture was stirred for 20minutes, followed by heating to 85° C. At 85° C., 1.06 g-of sodiumpersulfate dissolved in 25 g of water and 0.47 g of sodium carbonatedissolved in 25 g of were added to the reaction flask in a single shot,followed with 20 g of deionized water rinse. Following the charges ofinitiator and buffer, the reaction mixture was maintained with stirringat 85° C. for 60 minutes. After cooling the reaction mixture to 40° C.,13.72 g of a 0.15% solution of FeSO₄ in water was added with stirring,followed by additions of t-butyl peroxide and isoascorbic acid (0.70 gand 0.34 g each in 15 g of water, respectively). A second addition oft-butyl peroxide and isoascorbic acid in the same amounts were added 15minutes after the first one. The reaction mixture was held with stirringfor 30 minutes at a temperature of 40° C.

[0097] The resulting copolymer composition was cooled to roomtemperature and passed through a filter cloth to remove any coagulum.The resulting graft copolymer contained 64 weight percent of butylacrylate, 35 weight percent of methyl methacrylate and 1 weight percentof PMAA-MM. The copolymer composition had an incorporation of PMMA-MM of76 weight percent based on the total weight of PMMA-MM charged.

Example 9 Characterization of Copolymer Compositions

[0098] Graft copolymer compositions prepared in the previous exampleswere characterized by various analytical techniques to determine wt %solids, particle size, weight average molecular weight, number averagemolecular weight, and percent incorporation of macromonomer.

[0099] Determination of the amount of unreacted macromonomer was carriedout by HPLC analysis using the following procedure. The copolymercompositions were dissolved in THF and analyzed by gradient elution onan LC-18 column supplied by Supelco, located in Bellefonte, Pa. suchthat a well-isolated peak was observed for the unreacted macromonomer.Quantification was carried out by calibrating the detector responseusing known standards of the same macromonomer employed in thesynthesis. The results of the characterization are reported in Table 8below. TABLE 8 Characterization Of Copolymer Compositions ParticlePMMA-MM % Size Mw Mn Incorp.⁽²⁾ Example Solids (nm) (×10⁻³) (×10⁻³) (wt%) 3.1 C 43 120 ⁽¹⁾ ⁽¹⁾ <2 3.2 43.1 268 119.7 88.6 89 3.3 41.0 204 286.029.0 — 3.4 49.3 245 398.1 217.7 90 3.5 50.2 215 708.2 378.3 86 3.6 51.5228 1015.0 266.9 68 3.7 48.1 226 1242.6 809.6 74 3.8 47.5 215 1082.6827.4 71 3.9 42.2 180 724.9 114.2 — 3.10 41.3 203 1468.9 875.5 — 3.1139.6 208 1263.8 964.0 — 3.12 39.7 227 1226.1 813.1 — 3.13 43.5 232 226.188.8 83 3.14 44.6 208 795.8 182.0 75 3.15 44.4 220 437.1 160.3 88 3.1641.4 194 216.1 139.3 71 4.1 34 222 533.3 66.6 86 4.2 43.5 210 264.5 67.391 4.3 42.3 181 664.8 83.2 94 4.4 42.8 168 857.9 72.1 94 6.1 39.3 192552.0 328.0 — 7.1 33.1 161 98.7 20.7 60 8.1 44 150 1041.6 146.9 76

Example 10 Analysis of Example 3.16

[0100] A two-dimensional HPLC analysis was carried out on Example 3.16to determine the average number of grafts per polymer molecule and toshow that a graft copolymer is formed. Two-dimensional HPLC providesmuch greater resolution compared to conventional HPLC for the separationof complex polymer materials. The method used in this analysis wassimilar to that described in “2D Chromatographic Analysis Of GraftCopolymers Obtained By Copolymerization Of Macromonomers ViaConventional, Controlled Radical, And Anionic Polymerizations” byMüller, Axel H. E et al., Polym. Prepr., Am. Chem. Soc., Div. Polym.Chem., 40(2), pages 140-141, 1999, which is hereby incorporated byreference in its entirety. LCCC was used in one dimension and GPC wasused in the second dimension; cuts from the first analysis weresequentially analyzed by the second technique, and appropriate softwareconstructed a plot of the data in two dimensions. The LCCC analysis wasrun under critical conditions for PBA, and size exclusion conditions forPMMA so that the total molecular weight of the MMA grafts on thecopolymer could be determined. From this value, (assuming each sidechain contained one macromonomer) the number of side chains percopolymer was calculated. Also, LCCC was used to determine thecomposition of the copolymer. The analysis in the second dimension usingSEC was used to estimate the total molecular weights of the copolymer.The molecular weights measured were calibrated using standards of PMMAfor the LCCC dimension and PBA for the GPC dimension. The resultingtwo-dimensional chromatogram showed a major copolymer peak (roughlyestimated at >70%) which, from the LCCC data, contained a total PMMAmolecular weight (Mn) of about 110,000. Using the Mn value of 9600 forthe PMMA macromonomer, an average number of grafts per polymer chain wasestimated at about 11.5. From the second dimension the overall molecularweight of this peak was estimated to be 580,000. The two-dimensionalchromatogram showed two other series of copolymer peaks, but no PBAhomopolymer was detected. The overall composition of the major copolymerpeak calculated from the two-dimensional HPLC data was about 85 wt % BAand 15 wt % MMA. This composition varies from the expected compositionof 72 wt % BA and 28 wt % MMA (calculated from an NMR analysis of thecomposition, taking into account that only about 70% of the macromonomerwas converted to copolymer), but is reasonable considering thecomplexity of the copolymer system and the analysis of it.

Example 11 Evaluation Of Shear Stability Of Graft Copolymer Compositions

[0101] Shear stability tests were carried out on several graft copolymercompositions made in the previous examples. Shear stability was testedby placing a drop of the graft copolymer composition on the index fingerand rubbing the composition between the thumb and index finger. Acopolymer composition passed if it could be rubbed until it dried bywater evaporation without the formation of coagulum, and failed if itflocculated after a few rubs and became ropy. All of the copolymercompositions tested were stable colloidally under static conditions. Theresults are reported in Table 9 below. TABLE 9 Finger Rub Test Resultsfor Graft Copolymer Compositions Example Stabilized acid Finger Rub Test3.4 pMAA-MM Pass 3.5 pMAA-MM Pass 3.6 pMAA-MM Pass 3.7 pMAA-MM Pass 3.8pMAA-MM Pass 3.9 MAA Fail  3.10 MAA Fail  3.11 MAA Fail  3.12 MAA Fail4.1 pMAA-MM Pass 4.2 pMAA-MM Pass 4.3 pMAA-MM Pass 4.4 pMAA-MM Pass 8.1pMAA-MM Pass

[0102] The data in Table 9 shows that graft copolymer compositionsprepared with an acid containing macromonomer had surprisingly goodshear stability in comparison to graft copolymer prepared with an acidmonomer. It was also discovered that good shear stability could beobtained, without the use of an acid containing macromonomer, such as byadding a surfactant such as Triton™ X-405, a nonionic surfactantsupplied by Union Carbide, to the copolymer composition.

What is claimed is:
 1. A copolymer composition comprising waterinsoluble graft copolymer particles, wherein the graft copolymerparticles comprise: (a) from 2 weight percent to 90 weight percent ofmacromonomer, as polymerized units, based on the total weight of thecopolymer, wherein: (i) the macromonomer is water insoluble andcomprises from 10 to 1000 polymerized units of at least one firstethylenically unsaturated monomer, no polymerized mercapto-olefincompounds, and less than 5 weight percent polymerized acid-containingmonomer; and (ii) the macromonomer is a macromonomer prepared by aqueousbased polymerization; and (b) from 10 weight percent to 98 weightpercent of polymerized units of at least one second ethylenicallyunsaturated monomer, based on the total weight of the copolymer.
 2. Thecopolymer composition of claim 1 wherein the macromonomer comprises from20 to 200 polymerized units of at least one first ethylenicallyunsaturated monomer
 3. The copolymer composition of claim 1 wherein themacromonomer comprises as polymerized units less than 1 weight percentacid containing monomer, based on the total weight of the macromonomer.4. The copolymer composition of claim 3 wherein the copolymercomposition further comprises from 0.2 weight percent to 10 weightpercent of an acid containing macromonomer, or acid containing monomerbased on the total weight of the copolymer.
 5. The copolymer compositionof claim 4, wherein the acid containing macromonomer is attached to thesurface of the copolymer particles.
 6. The copolymer composition ofclaim 3 wherein the acid containing monomer is present, as polymerizedunits, in the acid containing macromonomer at 50 weight percent to 100weight percent, based on the weight of the acid containing macromonomer.7. The copolymer composition of claim 3 wherein the acid containingmonomer is present, as polymerized units, in the acid containingmacromonomer at 90 weight percent to 100 weight percent, based on theweight of the acid containing macromonomer.
 8. The copolymer compositionof claim 1 wherein the graft copolymer comprises a backbone and one ormore side chains, wherein the side chains are pendant from the backboneand comprise the water insoluble macromonomer, and wherein the backbonecomprises the polymerized units of the second ethylenically unsaturatedmonomer.
 9. The copolymer composition of claim 1 wherein the firstethylenically unsaturated monomer is an α-methyl vinyl monomer, a nonα-methyl vinyl monomer terminated with a α-methyl vinyl monomer, orcombinations thereof.
 10. The copolymer composition of claim 9 whereinthe first ethylenically unsaturated monomer is methyl methacrylate,ethyl methacrylate, 2-ethylhexyl methacrylate, isobornyl methacrylate,butyl methacrylate, lauryl methacrylate, stearyl methacrylate, styreneterminated by α-methyl styrene, or combinations thereof.
 11. Thecopolymer composition of claim 1 wherein the second ethylenicallyunsaturated monomer is selected from the group consisting of acrylateesters; methacrylate esters; styrene; substituted styrenes; olefinicallyunsaturated nitriles; olefinically unsaturated halides; vinyl esters oforganic acids; N-vinyl compounds; acrylamide; methacrylamide;substituted acrylamides; substituted methacrylamides;hydroxyalkylmethacrylates; hydroxyalkylacrylates; vinyl ethers; dienesand combinations thereof.
 12. The copolymer composition of claim 11wherein the second ethylenically unsaturated monomer is selected fromthe group consisting of C₁ to C₁₈ alkyl acrylate, styrene, butadiene,and combinations thereof.
 13. The copolymer composition of claim 1wherein the graft copolymer is a graft copolymer prepared by a methodcomprising: (a) forming a macromonomer aqueous emulsion comprising oneor more water-insoluble particles of the macromonomer, wherein themacromonomer has at least one terminal ethylenically unsaturated group;(b) forming a monomer composition comprising at least one secondethylenically unsaturated monomer; and (c) combining at least a portionof the macromonomer aqueous emulsion and at least a portion of themonomer composition to form a polymerization reaction mixture andpolymerizing the macromonomer with the second ethylenically unsaturatedmonomer in the presence of an initiator to produce a copolymercomposition comprising graft copolymer particles.